Lyondellbasell Icorene 3560 Bue 5759 Polyethylene Linear Low Density

LyondellBasell Icorene 3560 BUE 5759 Polyethylene, Linear Low Density

    • Product Name: LyondellBasell Icorene 3560 BUE 5759 Polyethylene, Linear Low Density
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 782272
    Product LyondellBasell Icorene 3560 BUE 5759 Polyethylene, Linear Low Density
    Color Blue
    Density 0.935 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 6.0 g/10 min
    Tensile Strength At Yield 10.0 MPa
    Tensile Strength At Break 12.0 MPa
    Elongation At Break 700%
    Flexural Modulus 300 MPa
    Shore D Hardness 50
    Vicat Softening Point 100 °C
    Melting Point 124 °C
    Deflection Temperature At 0 46 Mpa 50 °C
    Thermal Expansion Coefficient 2.0E-4 cm/cm/°C
    Specific Heat 2.3 J/g·°C
    Dielectric Constant 2.3
    Dielectric Strength 20 kV/mm
    Volume Resistivity >1E14 ohm·cm
    Water Absorption <0.01%

    As an accredited LyondellBasell Icorene 3560 BUE 5759 Polyethylene, Linear Low Density factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Supplied in 25 kg moisture-resistant polyethylene bags, palletized at 1,000 kg per pallet for safe transport and storage.
    Container Loading (20′ FCL) LyondellBasell Icorene 3560 BUE 5759 LLDPE loaded in 20′ FCL: 25 kg bags, palletized, shrink-wrapped, secured; approx. 20–22 MT net.
    Shipping LyondellBasell Icorene 3560 BUE 5759 Polyethylene, Linear Low Density is a non-hazardous thermoplastic resin. It is typically shipped in 25 kg bags, bulk bags, or octabins on pallets, or in bulk trucks/railcars. Store dry, away from heat, sunlight, and moisture; no special transport classification required.
    Storage Store LyondellBasell Icorene 3560 BUE 5759 LLDPE in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep original containers closed to prevent moisture and contamination. Avoid contact with strong oxidizers. Store indoors on pallets, off the floor. Use first-in, first-out stock rotation. Do not exceed recommended stacking heights to prevent bag deformation.
    Shelf Life Shelf life is typically 24 months from manufacture when stored in original unopened packaging, cool, dry, and protected from direct sunlight.
    Application of LyondellBasell Icorene 3560 BUE 5759 Polyethylene, Linear Low Density

    What Determines ESCR After Ferric Chloride Contact in Agricultural Water Tanks?

    During rotomolding of agricultural water tanks, the wall thickness between 4 mm and 8 mm must be controlled by shot weight, because the grade requires a peak internal air temperature of 190°C to 200°C to fully sinter the powder without allowing the mold face temperature to exceed 230°C for more than 4 min. Icorene 3560 BUE 5759 is pulverized to a particle size distribution with 95 wt% passing 35 mesh (500 µm) and no more than 1.5 wt% retained on 30 mesh (600 µm); a finer grind promotes surface densification but increases thermal degradation risk in the oven. The grade is rotationally molded on shuttle or carousel machines using a primary-to-secondary axis rotation ratio of 4:1. Oven set-points of 280°C to 300°C with forced air circulation are used, with total oven residence times of 18 min to 24 min for 5 mm nominal wall thickness. Terminal products include 500 L to 10,000 L cone-bottom fertigation tanks, horizontal agricultural water tanks, and sump bodies.

    Compliance for agricultural tanks is assessed under AS/NZS 4766:2006 for rotomolded polyethylene storage tanks, with chemical resistance validated by environmental stress-cracking resistance testing under ASTM D1693-15b in 10% Igepal CO-630 at 50°C. Where F50 values below 100 h are recorded, the formulation is unsuitable for aggressive fertigation service containing ferric chloride at 0.5 wt% to 1.0 wt%. The 5759 grade includes a hindered amine light stabiliser package; typical formulation practice adds 1.5 wt% to 2.5 wt% carbon black masterbatch for UV protection, 0.08 wt% to 0.15 wt% secondary antioxidant to widen the rework window, and 0.5 wt% to 1.0 wt% internal lubricant only if demolding of deep cone inserts becomes difficult. Mold release should be applied at no more than 0.2 g/m² to avoid weld-line porosity at the tank bottom. The resin is not suitable for continuous immersion in aromatic hydrocarbons, strong oxidizing acids, or sodium hypochlorite solutions above 5% free chlorine.

    Nominal wall thicknessOven set-pointPeak internal air temperatureForced-air cooling interval
    4 mm270–285°C185–190°C14–18 min
    6 mm280–295°C190–195°C18–22 min
    8 mm285–300°C195–200°C22–26 min
    10 mm290–310°C200–210°C26–32 min

    Because the LLDPE backbone of Icorene 3560 BUE 5759 provides lower crystallinity than HDPE alternatives, the grade can be rotationally molded into single-wall chemical containment units without the low-temperature brittleness that causes stress cracking in high-density polyethylene at -20°C. Industrial chemical containment processors pulverize the grade to a 35 mesh top cut and charge it into steel or cast aluminium molds with draft angles of 2° to 3°; corner radii below 20 mm are avoided because they concentrate residual hoop stress. Wall thickness is typically 5 mm to 8 mm, and the shot weight is established by trial on the specific mold rather than by a generic density factor, because published data for this specific configuration is limited. Oven set-points are 280°C to 295°C, with a peak internal air temperature of 190°C to 200°C and a primary-to-secondary rotation ratio of 4:1. Compliance is assessed under EN 13575:2012 for static thermoplastic tanks above ground; UN-certified chemical drums must additionally pass leakproofness, hydraulic pressure, and drop tests under 6.1.5.3 of the UN Model Regulations. The 5759 UV stabilizer package is normally sufficient; if annual ultraviolet exposure exceeds 40 kLy, 1.0 wt% to 2.0 wt% carbon black masterbatch is used. Additive levels above 3 wt% reduce ESCR; antistatic packages for solvent service are not recommended because they can accelerate strain hardening. Terminal products include 120 L to 1,500 L open-top drums, horizontal cylindrical tanks, secondary containment bunds, and chemical transfer totes.

    Municipal refuse container shells: cold impact at −20°C and UV stabilization

    Under EN 840-1:2020 drop test and cold-impact requirements, rotationally molded 80 L to 390 L two-wheeled refuse container shells are produced with nominal wall thicknesses of 3.5 mm to 5.5 mm. The powder is pulverized with a 35 mesh top cut and processed in shuttle machines at oven set-points of 270°C to 290°C, with the peak internal air temperature held at 185°C to 195°C. Undercure below 180°C produces brittle failures in the -20°C cold drop test because residual unmelted powder skins and catalyst particulates act as crack initiation sites. The 5759 UV package is generally adequate for 8,000 h of accelerated weathering under ISO 4892-2:2021; color masterbatch is added at 1 wt% to 2 wt%, but dark colors require a cooling rate reduction of 3°C/min to 5°C/min compared with natural resin to avoid panel distortion. Zinc stearate mold release is applied at 0.1 g/m² to 0.3 g/m²; higher release levels cause surface haze and reduce lid-hinge weld strength. Terminal products include 80 L, 120 L, 240 L, and 390 L two-wheeled municipal waste and recycling containers.

    At wall thicknesses above 8 mm, the cooling phase for rotomolded playground panels and urban furniture made from Icorene 3560 BUE 5759 must be staged to control post-molded warpage. A forced-air interval of 12 min at 0.3 m/s is used to lower the mold surface temperature from 180°C to 110°C, followed by 8 min of water mist at 0.1 L/min to reach 70°C; demolding proceeds only after the core drops below 50°C. Premature demolding of thick sections with a core temperature above 65°C causes warpage and reduces the impact attenuation performance required under ASTM F1487-21 and EN 1176-1:2017. The powder is charged into multi-part cast aluminium molds with three-dimensional inserts; primary rotation speed is reduced to 6 rpm and secondary speed to 1.5 rpm to prevent powder bridging in deep rib sections. Formulation practice for outdoor furniture includes 1.5 wt% to 2.0 wt% UV-resistant color masterbatch; brominated flame-retardant additives are avoided because they reduce UV stability and generate corrosive mold residues. Terminal products include slide enclosures, roof shells, seating shells, and structural playground panels.

    When Marine Buoyancy Shell Walls Exceed 10 mm, Crystallization Shrinkage Governs Weld Line Integrity

    If the peak internal air temperature overshoots 210°C in marine buoyancy shells, the excess exotherm accelerates crystallization shrinkage and creates weld-line tears because the wall thickness of 10 mm to 18 mm retains heat longer than thinner sections. Icorene 3560 BUE 5759 is therefore processed at oven set-points of 290°C to 310°C, with the peak internal air temperature maintained at 200°C to 210°C to ensure full sintering of the powder. Cooling must be slowed through the crystallization range of 110°C to 95°C to avoid sink marks and weld-line tears at the foam-filling ports. The mold rotation ratio is typically 3:1 to 4:1, with secondary axis speed held below 2 rpm for shells above 14 mm to minimize powder separation. No single universal standard governs marine buoyancy parts; classification society approval is issued case-by-case, and published data for this specific configuration is limited. The 5759 UV stabilizer is essential for saltwater exposure; black hull sections use 1.0 wt% to 2.0 wt% carbon black masterbatch to reduce gloss loss and chalking. Hydrophilic antistatic additives are excluded because moisture absorption can delaminate the rotomolded shell from closed-cell polyurethane foam cores. Amine-based foam catalysts must not contact the resin at temperatures above 40°C because the exotherm can accelerate oxidative degradation. Terminal products include mooring buoy shells, dock fender sleeves, and floating walkway pontoon skins.

    Cable junction boxes and underground enclosures are rotationally molded from Icorene 3560 BUE 5759 when impact toughness and moisture resistance are required in outdoor distribution networks. Enclosure protection is specified under IEC 60529:1989+A2:2013 for ingress protection ratings and EN 62262:2002 for impact resistance; IP66 and IP67 ratings are achieved through sealing geometry, not by the resin alone. Wall thickness is 3 mm to 5 mm, with oven set-points of 270°C to 285°C and a peak internal air temperature of 185°C to 195°C. Molds are designed with knockouts and insert bosses to avoid undercuts; metallic inserts are preheated to 120°C before loading to reduce shrinkage stress. If electrostatic dissipation is required, conductive carbon black is added at 8 wt% to 15 wt%, a loading that reduces tensile elongation by approximately 40% and requires reprocessing parameter adjustments. The base 5759 grade is naturally non-conductive; no claim of surface resistivity improvement should be made for the unmodified material. Terminal products include ground boxes, splice enclosures, telecommunications handholes, and connection pit covers.

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    Certification & Compliance
    More Introduction

    LyondellBasell Icorene 3560 BUE 5759 is a linear low density polyethylene supplied as a powder for rotational molding. The grade identifier 3560 and the suffix BUE 5759 identify the base resin, melt flow position, UV-stabilizer package, and colour configuration. Manufacturer technical data sheets for this powder typically report a density near 0.935 g/cm³ when tested under ISO 1183-1 and a melt flow rate near 6.0 g/10 min at 190 °C under a 2.16 kg load as specified in ISO 1133-1. Because the product is a linear low density polyethylene, short-chain branching is introduced by alpha-olefin comonomer incorporation along a predominantly linear backbone. The absence of long-chain branching typically reduces melt elasticity relative to high-pressure LDPE while increasing solid-state toughness and environmental stress-crack resistance at comparable density.

    As a rotomolding powder, the product is not pelletized. Dry-flow behaviour, bulk density, and particle size distribution are therefore as process-critical as melt flow rate. The powder form allows the material to coat mold surfaces under biaxial rotation before a continuous melt film develops. Production-scale experience with shuttle and carousel machines indicates that moisture uptake above 0.05 wt% can reduce dry-flow and create uneven wall thickness in molds with deep pockets, narrow ribs, or long pinch-off zones.

    Typical end-use fields include rotationally molded storage tanks, agricultural hoppers, equipment housings, chemical containment liners, and outdoor recreational components. The combination of medium density and a melt flow rate of 6.0 g/10 min suits medium-wall parts in the 3–12 mm thickness range. For complex geometries, mold-dependent factors such as venting, surface texture, and rotation path influence the final wall-thickness distribution as much as the resin itself.

    What Limits Oven Cycle Time in Rotational Molding with This Grade?

    Oven cycle time is governed by peak internal air temperature, not by a fixed residence time. Typical rotomolding ovens for LLDPE operate at air temperatures of 280–320 °C. The powder progresses through tackification, sintering, densification, and bubble removal; peak internal air temperature commonly reaches 200–240 °C before the part is removed from the oven. If peak internal air temperature remains below 190 °C, the inner surface may contain residual porosity and incompletely healed polymer particles. If peak internal air temperature exceeds 260 °C, thermo-oxidative degradation accelerates and discolouration can become visible, particularly in non-black packages such as BUE 5759.

    On multi-arm carousel lines with arm ratios of 4:1 and swing diameters near 1.5 m, wall thickness above 8 mm commonly requires a stepped oven profile: high initial heat input to sinter the outer skin, followed by reduced air temperature to allow through-thickness heating without overheating the inner surface. Published data for this specific configuration is limited; cycle settings should be established by instrumented mold trials using internal air temperature probes and thermocouples inserted through the mold wall.

    In biaxial rotation, wall-thickness distribution is controlled by the speed ratio between the major and minor axes. For symmetrical parts, a major-to-minor axis speed ratio of 4:1 to 5:1 is typical. Complex molds with deep pockets may require a ratio near 2:1 or non-uniform servo-driven rotation. Premature release of trapped air can appear as pinholing when the major axis speed is too high; a slower major axis or additional venting usually corrects the defect.

    Cooling also influences warpage and low-temperature toughness. Forced air cooling from 120 °C to below 60 °C is used to limit shrinkage and improve demolding. For large flat panels, slow cooling in still air may reduce warpage but increases cycle time. The balance depends on part geometry; production lines generally maintain cooling air temperature above the polymer crystallization range until dimensional stability is achieved.

    Powder Dry Flow and Particle Size Distribution Effects

    Rotomolding powders require controlled particle size distribution to flow into corners and through narrow mold passages. The Icorene 3560 BUE 5759 powder is supplied in a spherical or near-spherical particle form. Typical LLDPE rotomolding powders show median particle sizes between 150 µm and 500 µm, with bulk densities commonly in the range 350–450 kg/m³. Dry-flow time below 35 s/100 g is generally expected for uniform mold filling. Coarse particles retained on a 500 µm sieve can produce pinpoint voids at the outer mold surface; excessive fines below 150 µm can increase dust accumulation and complicate venting. Sieve analysis should be performed under ASTM D1921 or ISO 4610 on incoming material. Because dry-flow is sensitive to storage humidity, the powder should be stored at 20–25 °C and 50% RH wherever possible.

    In solid-state performance, a rotomolding LLDPE of this class typically exhibits tensile yield strength of 15–18 MPa under ISO 527-2 and flexural modulus of 550–750 MPa under ASTM D790. Elongation at break usually exceeds 800% for unfilled specimens. Impact resistance is a primary reason for selecting linear low density polyethylene over high density polyethylene in rotomolded tanks and equipment housings. Instrumented puncture testing under ISO 6603-2 may show ductile failure at -40 °C for wall thicknesses above 3 mm. Environmental stress-crack resistance under ASTM D1693-15 condition B in 100% Igepal CO-630 typically exceeds 1000 h; this value is substantially higher than unmodified high-pressure LDPE and comparable to many high-molecular-weight HDPE grades, although flexural modulus remains lower than that of HDPE.

    Density is a principal variable separating this grade from other LLDPE rotomolding resins. At 0.935 g/cm³, the stiffness-to-toughness balance is shifted toward stiffness relative to lower-density LLDPE grades near 0.930 g/cm³, and toward toughness relative to higher-density grades near 0.940 g/cm³. The melt flow rate also differs from lower-flow rotomolding grades that may be selected for very thick chemical tanks where extended oven cycles are acceptable. The higher-flow 3560 BUE 5759 is suited to medium-wall parts because it can fill complex mold details at lower peak internal air temperature, but it may show slightly lower low-temperature impact at equivalent density compared with lower-MFR variants.

    The BUE 5759 suffix denotes an ultraviolet-stabilized, non-black colour package. Conventional LLDPE exposed to natural weathering loses elongation through tie-molecule scission and carbonyl formation. Xenon-arc testing according to ISO 4892-2:2013 cycle 1 is used to screen UV stabilization. A stabilized rotomolding LLDPE of this class typically retains at least 70% of initial tensile elongation after 2000 h, but field service life depends on part thickness, orientation, and incident UV dose. Carbon black at 2.0–2.5 wt% remains the reference stabilizer for long-term outdoor service; BUE 5759 offers a coloured alternative but should not be assumed equivalent to carbon black for service beyond 10 years without outdoor exposure data from the specific part geometry.

    A Narrower Molecular Weight Distribution Than High-Pressure LDPE

    The structural difference between Icorene 3560 BUE 5759 and high-pressure LDPE is molecular architecture. High-pressure LDPE contains long-chain branches that increase melt strength and reduce melt flow under extensional stress. This LLDPE product has a predominantly linear backbone and short-chain branches, which improves tensile strength, puncture resistance, and environmental stress-crack resistance but reduces melt elasticity. In film extrusion, lower melt strength can be a processing disadvantage; in rotational molding, melt strength is less critical because the polymer is supported by the mold surface. The table below compares class-typical values for LLDPE, LDPE, and HDPE rotomolding resins. The entries are broad material-class values and not specification limits for the Icorene grade.

    PropertyLLDPE rotomolding classHigh-pressure LDPEHDPE rotomolding homopolymerTest method
    Density0.930–0.940 g/cm³0.917–0.930 g/cm³0.945–0.965 g/cm³ISO 1183-1
    Melt flow rate at 190 °C/2.16 kg5–7 g/10 min4–8 g/10 min3–7 g/10 minISO 1133-1
    Tensile yield strength15–18 MPa8–12 MPa23–30 MPaISO 527-2
    Flexural modulus550–750 MPa200–350 MPa900–1200 MPaASTM D790
    Environmental stress-crack resistance>1000 h<100 h10–100 hASTM D1693-15

    Against HDPE rotomolding homopolymers, the LLDPE grade is lower in stiffness and heat deflection temperature but higher in low-temperature impact resistance and environmental stress-crack resistance. HDPE may be selected for structural parts requiring higher modulus or improved creep resistance at elevated temperature; LLDPE is selected for parts requiring ductile failure and resistance to cracking in the presence of detergents, agricultural chemicals, or mineral acids. Against metallocene-catalysed LLDPE, conventional Ziegler-Natta LLDPE may have a broader molecular weight distribution. That broader distribution often improves powder dry-flow and low-shear processability at the expense of slightly lower dart impact and clarity. If the base resin in Icorene 3560 is Ziegler-Natta, these differences should be evaluated through melt rheology under ISO 3219 and gel permeation chromatography before substitution. Published data for this specific configuration is limited.

    When Peak Internal Air Temperature Exceeds 260°C

    At peak internal air temperature above 260 °C, the antioxidant package is consumed rapidly and the non-black BUE 5759 formulation may show yellowing, inner-surface oxidation, and a decline in impact resistance. Oxidation induction time measured under ISO 11357-6 at 200 °C is a practical incoming-resin control. A reduction of oxidation induction time below 20 min indicates that the stabilizer package is approaching depletion. For thick sections, the inner surface may remain above 200 °C after demolding; cooling air should continue to extract heat until the core drops below 90 °C to reduce post-molding oxidative exposure.

    Venting must remain open to avoid pressure-generated blow holes; a blocked vent can raise internal pressure and force molten polymer through the parting line. The powder should not be pre-dried above 70 °C in a forced-air oven because partial melting can cause agglomeration and loss of dry-flow. When regrind is used, repeated heat histories consume the primary antioxidant; regrind additions above 20 wt% are not recommended unless oxidation induction time and impact testing confirm equivalent durability.

    Chemical resistance follows general polyethylene behaviour. The material resists dilute acids, alkalis, and aqueous salt solutions at moderate temperature, but concentrated oxidizing acids, chlorinated hydrocarbons, and low-boiling aromatic solvents can swell or degrade the surface, especially at elevated service temperatures. The BUE 5759 UV package may influence colour stability in contact with certain agricultural chemicals; compatibility testing should follow ISO 175 immersion procedures.

    Regulatory declarations are required for any end-use statement. Polyethylene copolymers for food contact may be evaluated under FDA 21 CFR 177.1520, but the BUE 5759 colour and UV package must be included in the extraction testing and end-use limitations. For European food contact, overall migration under EU 10/2011 must not exceed 10 mg/dm². REACH Annex XVII and RoHS 2011/65/EU obligations attach to the specific additive formulation, with 0.1% w/w as the general RoHS threshold for lead, mercury, hexavalent chromium, polybrominated biphenyls, and polybrominated diphenyl ethers; the cadmium threshold is 0.01% w/w. A supplier declaration should be obtained for each lot because the UV stabilizer and colourant package determines compliance.

    Operational boundaries require attention to moisture, contamination, and regrind. At ambient relative humidity above 60%, pre-drying in a dehumidified hopper at 40–50 °C for 2–4 h is advisable to restore dry-flow, though the powder should not be heated above 70 °C. Regrind addition should be limited to 20 wt% unless process validation demonstrates equivalent impact resistance, because repeated oven cycles consume the primary antioxidant. Incompatible additives include strong Lewis acids and certain amine-based antistatic packages that can accelerate discolouration in non-black rotomolding powders; compatibility should be confirmed by oxidation induction time testing under ISO 11357-6 before production.

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